Loop Reactor for Emulsion Polymerisation

ABSTRACT

A polymerization reactor comprising a circulation loop, an inlet for raw material, an outlet, driving means for circulating a reactor charge within the circulation loop, and a pig station for storing, launching, and receiving cleaning pigs. The pig station comprises a lid to cover an opening enabling removal of the cleaning pig. The pig station is constructed as a box with a cylindrical bore connected at both ends to the circulation loop, the bore having a central part with a diameter which is larger than the inner diameter of the circulation loop. At a transitional part at the outer ends of the bore the bore diameter narrows down to be substantially equal to the inner tube diameter of the circulation loop. Over at least a part of the inner bore substantially half of the circular cross-section is formed in the removable lid.

RELATED APPLICATIONS

This is a continuation of U.S. application Ser. No. 11/666,974, filed onJun. 28, 2007, which claims priority from PCT/EP2005/055619, filed onOct. 28, 2005, which claims priority from EP Application Serial Number04256745.3, filed on Nov. 2, 2004, the contents of each are herebyincorporated by reference in their entirety.

FIELD

The present invention relates to a polymerization reactor comprising oneor more circulation loops with one or more inlets for raw material, oneor more outlets, driving means for circulating a reactor charge withinthe circulation loop, and a pig station for storing, launching, andreceiving cleaning pigs.

BACKGROUND

WO 00/07177 discloses a loop reactor for emulsion polymerization. Theloop reactor comprises a circulation pump and a tubular circulation loopconnecting the pump's outlet to its inlet. Water, monomers, andstabilizers are continuously fed to the loop and circulated and polymeremulsion is continuously drawn off. The reactor is particularly suitablefor the production of polymers derived from vinyl and/or acrylicmonomers, used for instance in paints or adhesives.

A problem encountered in polymerization processes employing a tubularreactor is the formation of deposits from the reaction products on theinternal wall of the reactor. These deposits lead to a need for anincreased delivery pressure from the circulation pump and impair heattransfer from the reaction medium to, e.g., a coolant in a jacketsurrounding the reactor tube, thus leading to higher and oftendeleterious reactor temperatures or else necessitating an increasedcoolant circulation rate, a lower coolant temperature, or a reduced rateof production. Fouling also reduces the reactor volume, increasing boththe recycle rate and the shear on the emulsion. This shifts the processconditions, which may have been optimized on a clean reactor. In anycase, product properties will drift, nullifying the advantages ofconsistency of production expected from continuous reactors. In WO00/07177 cleaning pigs are used for cleaning the inside of the reactortubes. The cleaning pigs have a diameter which is about the innerdiameter of the reactor tube. The pigs are launched from a pig stationand propelled through the loop by the polymerizing emulsion.

A drawback of this prior art system is that the pigs cannot be easilyreplaced when they are worn out. A whole section of tubing in which thepig comes to rest, must be removed, resulting in loss of emulsion andsoiling of equipment. Further, it is difficult to manufacture a tubesection which fits exactly in such a way that only a small force wouldslide it out when the section is uncoupled to take out the pig andconversely slide it back in after maintenance on the pig. If the tube isfractionally too long it is difficult to remove and replace and if tooshort there is difficulty in sealing to the other pipes. Moreover, thereis a general difficulty in designing a removable tube that does not leakpolymer emulsion.

SUMMARY

The object of the invention is to provide a pigging station allowingquick and frequent launching of cleaning pigs and easier and fasterreplacement of cleaning pigs, without spill of emulsion.

The object of the invention is achieved by a tubular reactor with a pigstation comprising a lid to cover an opening enabling removal of thecleaning pig. This way, removal and replacement of the pig can be donewithout interruption of the production process being necessary. To alloweasier removal, the opening can be larger then the length of the pigsand have a width which is at least equal to the largest diameter of thepig.

In an optional embodiment, the pig station comprises a box with acylindrical bore connected at both ends to the circulation loop, thebore having a central part with a diameter which is larger than theinner diameter of the circulation loop. In a transitional part at theouter ends of the bore the bore diameter narrows down to besubstantially equal to the inner tube diameter of the circulation loop.The transitional part can be part of the connected tube part or can be aseparate part. Preferably, the transitional part is an integral part ofthe pig station.

Due to the enlarged bore diameter, polymer emulsion in front of the pigcan flow backwards around the pig.

In the rest position, the front of the pig is positioned against thebevel of the transitional part joining the larger diameter section inthe box to the smaller diameter of the tube forming the circulationloop. Thus the pig is forming a seal at its front end. By virtue of thisseal, the pig is forced to move into the circulation loop when waterphase is diverted to enter the pig box at a point behind the pig. At theother end of the sequence when the pig is returning, the driving forceis provided by polymer emulsion which has been temporarily diverted viathe box. Liquid in front of the pig is allowed to move backwards pastthe pig via the gap provided by the larger diameter of the cavity in thepig box. The volume of emulsion pushing the pig is more than sufficientto move the pig forward even though some of it can pass along the gap.The length of the pig can be adopted such that when the pig has come toa halt, its front end is sealed at the bevel end and the pig is in thecorrect position for another launch.

Preferably, half of the circular cross-section is formed in theremovable lid.

The pig station can be incorporated into a branch of the circulationloop, e.g., in a by-pass line by-passing the driving means. To divertthe pig from the main flow of emulsion to the pig station, a divertercan be used. The diverter can be a bar or a pin hingable between anormal operating position, allowing full bore flow of emulsion, and adiverting position, diverting the pig to the pig station. A suitableexample of such a diverter is described in GB-A 2,196,716. The diverteris preferably electronically actuated, e.g., in response to a pigdetector located upstream.

The reactor can comprise a shut-off valve behind the pig station to stopthe flow of emulsion via the pig by-pass after the pig has returned toits starting position. The reactor can additionally comprise a by-passline for by-passing reactor charge around the shut-off valve.

Optionally, the inner bore is in open connection with a water phasefeed. This allows an easy and fast launch of the pig by water phase. Inthat case, the reactor can comprise a shut-off valve to stop the waterphase feed into the pig box after the pig is launched.

The closed loop reactor can comprise a reactor tube of which at least asubstantial part forms a helical coil. In comparison to the commontrombone arrangement of the continuous tube (as disclosed in, e.g., M.Wilkinson and K. Geddes, “An award winning process,” Chemistry inBritain, pp. 1050-1053, December 1993), the shape is more appropriatefor pigging in that the pig is not forced to make sharp turns, thusreducing the wear of the pig and allowing the use of longer pigs.Furthermore, uncooled joints, which are one of the origins of wallfouling, can be avoided by using a helically coiled continuous tube.

A pig can be launched at intervals ranging from approximately 1 toapproximately 60 minutes, preferably from approximately 10 to 20minutes. Apart from more effective cleaning of the tube walls, regulardisturbance of slow moving or static layers of emulsion polymer close tothe tube walls will prevent the onset of a stationary layer of polymerwhich is a poor heat conductor.

Some typical monomers suitable for use in the present polymerizationprocess include, e.g., butyl acrylate, methyl methacrylate, styrene,vinyl acetate, Veova® 9, Veova® 10, Veova® 11 (all three ex Shell),ethyl acrylate, 2-ethyl hexyl acrylate, ethylene, and vinyl chloride.The addition reaction is initiated by radicals to give a dispersion ofhigh-molecular weight polymer particles, usually of 50 to 3000 nmdiameter, suspended in a medium in which the polymer is insoluble,usually water. Common free radical generators include the sodium,potassium, and ammonium salts of peroxodisulphuric acid, e.g. ammoniumperoxodisulphate. Alternatively, redox couples can be used. Theseconsist of an oxidizing agent and a reducing agent. Commonly usedoxidizers are the salts of peroxodisulphuric acid and t-butylhydroperoxide and hydrogen peroxide itself. Reducers are sodiumsulphite, sodium metabisulphite, sodium formaldehyde sulphoxylate, andsodium dithionate.

Polymerization of monomers can take place in aqueous suspension and, inthat case, raw materials are preferably provided by separate feedstreams. These streams introduce fresh monomer and an aqueous solutionof stabilizers known as the water phase or, e.g., a pre-emulsion ofmonomer and water and an aqueous solution in a separate small stream. Atthe start of the reaction the reactor is filled with water phase made upin a solution tank. Other fillings are also possible, particularlyfinished emulsion polymer (of the same or different composition) from aprevious run, optionally diluted to any concentration.

Agitation in the reactor is provided by virtue of the in-linecirculation pump.

Shortly after the feed streams start to flow, the monomers begin toreact and heat is generated. The temperature is stabilized by coolingmeans, usually by controlled circulation of a cooling fluid (e.g. water)through a cooling jacket. The product flows to the cooling tank, whereresidual monomer converts to polymer. After cooling, the emulsionpolymer is filtered to remove any oversize particles or gritty materialin the strainer and transferred to the product storage tank.

Optionally, the polymerization process may be carried out underpressure, for instance under a pressure of 10 to 150 bar. Alternatively,the polymerization may be carried out at ambient pressure.

Pigs can for example be made of soft or semi-hard natural or syntheticmaterial, e.g. rubber or polyurethane. Also, pigs or scrapers with(flexible) metal parts or metal brushes as well as combinations of metaland a soft or semi-hard natural or synthetic material can be used. Ofthe numerous possible shapes, cylinders, cylinders with round edges aswell as cylindrical bodies with thick lips and/or thick strips on theouter circumference are particularly suitable. Dumb-bell shapedcylindrical pigs have two scraping surfaces, as opposed to sphericalsurfaces, which have only one.

The design of the pig and the materials used depend, among other things,on the type of deposit and the tolerances and radii of the reactor tube.Incidentally, it is noted that the amount of wear of the pig can bedetermined from the time needed for one cleaning cycle, since a worn pigwill require more time to complete a cycle. Suitable circulation pumpsare for instance positive displacement pumps.

BRIEF DESCRIPTION OF THE DRAWINGS

The invention is further illustrated by the drawings. In the drawings:

FIG. 1 shows a loop reactor according to the invention;

FIG. 2 shows a cross-section of the pig box of the loop reactor in FIG.1,

FIG. 3 shows a plan view of the pig box of the loop reactor in FIG. 1;

FIG. 4 shows a front view of the removable lid for a pig box as shown inFIGS. 2 and 3;

FIG. 5 shows a plan view of the lid of FIG. 4;

FIG. 6 shows a side view of the lid of FIG. 4;

FIG. 7 shows the valve arrangement around the pig box of FIG. 2; and

FIG. 8 shows a pig in a pig box, shown in cross section.

DETAILED DESCRIPTION

FIG. 1 shows a loop reactor 1. The reactor 1 comprises a circulationloop 2 with a monomer inlet 3, a water phase inlet 4, and an outlet 5for finished product. A circulation pump 6 serves as a driving means forcirculating a reactor charge within the circulation loop 2. A by-passline by-passes the pump 6 and includes a pig station 7 for storing,launching, and receiving cleaning pigs. In stream direction, the monomerfeed is located after the pump in order to reduce monomer content, andthus fouling rate, in the pump 6.

The pig station 7 comprises a pig box 8 as shown in cross-section andplan view in FIGS. 2 and 3, respectively. The pig box 8 comprises aninner bore 9 which is circular in cross-section, with a diameter whichis slightly larger than the diameter of the used pigs. At its upper end,the box 8 has an opening 10 which can be closed off by a removable lid(see FIG. 4). This opening 10 uncovers a semi-cylindrical recess 11. Theopening 10 and recess 11 are bordered by transitional parts 12, having acentral bore 13 in register with the recess 11. The inner diameter ofbores 13 narrows down to the outer ends to become equal to the innerdiameter of the connected loop tube 2.

Threaded holes 14 are provided to engage fastening means for fasteningthe removable lid. A cylindrical opening 15 is at right angles with therecess 11 and serves to discharge emulsion. Opening 16 serves as a feedfor water phase to launch a pig. Opening 16 may alternatively bepositioned directly into the pipe leading into the pig box. Opening 17serves to depressurize the pig box and drain prior to opening the lid.

The opening 10 of the pig box 8 can be closed off with a removable lid18, as shown in FIGS. 4, 5, and 6. The lid 18 can be fastened withregular fastening means through openings 19, which are in line with thethreaded holes 14 in the pig box 8 after the lid 18 is put in place. Thelid 18 comprises a top plate 20 provided with a central slot 21, whichserves to enable a magnet detector to be positioned closer to themagnets held in the body of the pig. This ensures detection when the pigre-enters the box after the circuit has been completed.

At one side of the top plate 20 the lid 18 comprises a block 22 with asemi-cylindrical recess 23. The recess 23 has the same diameter asrecess 11 in the pig box 8. When the lid 18 is put in place on the pigbox 8, recess 23 and recess 11 form a cylindrical bore. A secondsemi-cylindrical recess 24 in the lid 18 is at right angles with recess23. This recess 24 has the same diameter as bore 15 in the pig box 8 andis in line with bore 15 when the lid is placed on the pig box 8.

FIG. 7 shows a by-pass line 25 in a loop reactor according to theinvention for by-passing cleaning pigs around a circulation pump 27. Theby-pass line 25 includes a pig station 28 comprising a pig box 8 with alid 18 as shown in FIGS. 2-6. The pig station 28 is connected to a waterphase feed 31 and an emulsion discharge line 32, which leads to acollection tank (not shown). The water phase feed 31 has a first branch33, which leads to the circulation pump 27 and is provided with a firstshut-off valve 34, and a second branch 35, which leads to the pigstation 28 and is provided with a second shut-off valve 36. Near the pigbox, the discharge line 32 splits into a first branch 37 connected tothe by-pass line 25 at a location which is situated in flow directionbefore the pig station 28, and a second branch 38 connected to the pigstation 28. A third shut-off valve 39 is located in the first branch 37of the discharge line 32, a fourth shut-off valve 40 is located betweenthe pig station 28 and the location where the first branch is connectedto the by-pass line 25. A fifth shut-off valve 41 is located in thesecond branch 38 of the discharge line, while a sixth shut-off valve 42is located in the part of the by-pass line 25 which is situated in flowdirection past the pig station 28.

In normal use, the shut-off valves 34 and 39 are open, while the valves36, 40, 41, and 42 are closed. Part of the circulating emulsion isdischarged from the loop via the by-pass line 25, valve 39, and thedischarge line and collected in the collection tank, while fresh waterphase enters the loop via valve 34 and the circulation pump.

To launch the cleaning pig, first valves 42 and 36 are opened. Thenvalve 34 is closed. The fresh water phase is directed to the back of thepig in the pig box, pushing the pig out of the pig box into the loopcoil. An electromagnetic detector, located in the loop just past theby-pass line 25, notes when the pig passes it and initiates the openingof valve 34 and the shutting of valves 36 and 42. The pig goes aroundthe reactor circuit. Where the loop splits into the bypass line 25 andthe line leading to the circulation pump, the loop is internallyprovided with a diverter pin, which hinges between a first positionguiding the pig into the by-pass line, and a second position. Thediverter pin is under the control of a second electromagnetic pigdetector which is located just before the by-pass line 25. When itdetects a passing pig, it causes the diverter to hinge to the firstposition, guiding the pig into the by-pass line 25. Valves 40 and 41 areopened and valve 39 is closed. This re-routes the emulsion via the pigbox. A third electromagnetic pig detector, is located at the pig box anddetects the return of the pig, initiating the opening of valve 39 andthe closing of valves 40 and 41.

FIG. 8 shows a pig 43 in a pig box 8, in cross section. The pig 43 has acylindrical body 44 and two rubber ring scrapers 45 with a diameterwhich is equal to the inner diameter in the loop tubes, in order tocompletely clean the inner sides of the tubes and remove fouling. Theinner diameter of the central cylindrical bore 46, formed by recesses 11and 22, respectively, is larger than the inner tube diameter. As aresult, emulsion can flow backwards past the pig without hindering thepig in taking its starting position.

While the present inventions have been described in connection with anumber of exemplary forms, and implementations, the present inventionsare not so limited, but rather cover various modifications, andequivalent arrangements, which fall within the purview of the presentclaims.

1. A polymerization reactor comprising one or more circulation loopswith one or more inlets for raw material, one or more outlets, drivingmeans for circulating a reactor charge within the circulation loop, anda pig station for storing, launching, and receiving cleaning pigs,wherein the pig station comprises a lid to cover an opening, whichenables removal of the cleaning pig.
 2. The reactor according to claim1, wherein the pig station comprises a box with a cylindrical boreconnected at both ends to the circulation loop, the bore having acentral part with a diameter which is larger than the inner diameter ofthe circulation loop, and in a transitional part at the outer ends ofthe bore the bore diameter narrows down to be substantially equal to theinner tube diameter of the circulation loop.
 3. The reactor according toclaim 2, wherein for at least a part of the bore substantially half ofthe circular cross-section is formed in the removable lid.
 4. Thereactor according to claim 1, wherein the pig station is incorporatedinto a branch of the circulation loop and wherein the circulation loopcomprises a diverter diverting the pig to the pig station.
 5. Thereactor according to claim 4, wherein the pig station is incorporatedinto a by-pass line by-passing the driving means.
 6. The reactoraccording to claim 1, wherein the reactor comprises a shut-off valvebehind the pig station.
 7. The reactor according to claim 2, wherein thebore is in open connection with a water phase feed.
 8. The reactoraccording to claim 7, wherein the reactor comprises a shut-off valve inthe water phase feed of the pig box.
 9. The reactor according to claim2, wherein the transitional part is an integral part of the pig station.10. The reactor according to claim 2, wherein the reactor comprises ashut-off valve behind the pig station.
 11. The reactor according toclaim 3, wherein the reactor comprises a shut-off valve behind the pigstation.
 12. The reactor according to claim 3, wherein the bore is inopen connection with a water phase feed.
 13. The reactor according toclaim 12, wherein the reactor comprises a shut-off valve in the waterphase feed of the pig box.
 14. The reactor according to claim 4, whereinthe pig station comprises a box with a cylindrical bore connected atboth ends to the circulation loop, the bore having a central part with adiameter which is larger than the inner diameter of the circulationloop, and in a transitional part at the outer ends of the bore the borediameter narrows down to be substantially equal to the inner tubediameter of the circulation loop.
 15. The reactor according to claim 14,wherein for at least a part of the bore substantially half of thecircular cross-section is formed in the removable lid.
 16. The reactoraccording to claim 14, wherein the reactor comprises a shut-off valvebehind the pig station.
 17. The reactor according to claim 14, whereinthe bore is in open connection with a water phase feed.
 18. The reactoraccording to claim 17, wherein the reactor comprises a shut-off valve inthe water phase feed of the pig box.
 19. The reactor according to claim6, wherein the pig box is in open connection with a water phase feed.20. The reactor according to claim 19, wherein the reactor comprises ashut-off valve in the water phase feed of the pig box.